Method for comprehensively processing brown coal and leonardite into humic fertilizers and preparations and into fuel briquettes, and mechanochemical reactor for processing highly-viscous media

Abstract

A method for comprehensively processing coal-type caustobiolites, predominantly brown coal and leonardite, into humic organic and organomineral fertilizers and intor preparations producing fuel briquettes, including carrying out main processes in a continuous flow; carrying out leaching processes based on aqueous solutions with hydromodules of close to 2, carrying out acidification processes with the formation of humic acid released from a liquid phase into a heavy phase of a coagulated pulp, carrying out mechanical phase separation processes in a centrifugal field, carrying out liquid-phase mechanoactivation and the dispersion of reaction compositions via grinding, using residual “water” in recycling, and including the production of water-soluble humic acids and fuel briquettes and allowing for the production of a wide range of products; preliminarily grinding raw materials to a 03 mm class, and cleaning and electrochemically softening water in preparing reaction aqueous solutions; using a liquid-phase raw material oxidation process, and using liquid-phase mechanoactivation and / or mechanochemical activation, with the dispersion of reaction compositions by means of grinding and by means of dynamically shifting layers having statistical shift rate components, of a medium to be processed, which range from single-digit meters per second to tens of meters per second; accompanying said mechanoactivation with the dosed input into said medium of 1040 MJ of mechanical energy per cubic meter, with the stabilization of said dosing regardless of the drift of all other parameters in said medium to be processed; wherein, said grinding and shifting processes are formed by means of statistical and dynamic characteristics; in this way, a dynamic hydro-pulse effect on a medium to be processed is carried out within a range of frequencies floating between infrasound and frequencies bordering on ultrasound, wherein the processing is carried out beginning with higher frequencies; in addition, providing for automatically maintaining maximum parameters for inputting mechanical energy into the medium to be processed, while automatically restricting same within a sub-cavitation zone in order to prevent the transition of the mechanochemical reactors into cavitation modes.

Description

[0001]The requirement for the environmental safety of humankind on the planet defines not only the dynamics, but also the structure of foodstuffs. Significant growth of the share of foodstuffs produced without using mineral fertilizers or with limited use of them has been observed in recent years in the global production of agricultural products. A certain trend of rejection of foodstuffs of animal origin whose recovery is associated with the use of antibiotics and biostimulants has also been observed. Processes with the use of humates are a well-known, true-and-tried alternative that is already in use in comparison with the established agricultural industry processes.[0002]Owing to the biological activity of humic substances (HSs), they are used as plant growth stimulants or as microfertilizers. HSs are used successfully as soil conditioners and ameliorants while also activating the activities of soil microorganisms. HSs can be used as detoxicating agents in contaminated territorie...

AI Technical Summary

Benefits of technology

The patent text explains that humins are a type of organic substance found in soil. Humins are not soluble in water, but they can exist in different forms at different pH levels. They play important roles in soil by retaining water, improving soil structure, and stabilizing soil. They also help to exchange cations and improve fertility. Overall, humins are critical to the quality and health of fertile soil.

Problems solved by technology

In practice, it results in the fact that processes of strong mechanodestruction of the components being converted at large cavitation energies, and useful substances are destroyed.

Such a restriction is introduced due to the fact that sometimes ultrasound processing, including cavitation processing, may have a significant negative effect [18, 19].

Moreover, this acid hinders the growth of mold and some bacteria.

The reasons impeding the technical result being obtained in comparison with the solutions for invention [75]:the inability to arrange the conversion of the reaction components of anomalously viscous flowing media due to the fact that no special design and process solutions are envisaged for it;the design solution of the device allows for the ingression of the media being converted through rotor axial holes into the space between the rotor and the case of the device, which may result in rotor drive overloads, the overheat of the structure and in the jamming of the rotor;the lack of the opportunity to introduce the second component in liquid form into the device for conversion, with intensive mixing of the components, disperse and mechanically activate them with their greater localized mass transfer;the lack of functionally connected regulated rotor drive speeds and the regulation of mass feed of components for conversion to ensure the optimization of the modes of this conversion and to prevent the device from switching to cavitation mode by controlling acoustic noises in the media being converted.

The reasons impeding the technical result being obtained in comparison with the solutions for invention [78]:inability to convert the reaction components of anomalously viscous flowing media due to the fact that no special design and process solutions are envisaged for it;the solution aimed towards the prevention of the ingression of the media being processed via rotor axial holes into the space between the rotor and the case of the device (the chamber in the form of a taper lead) is an attempt to solve the problem but does not fulfill this function reliably enough, as gaps “remain” for the potential ingression of the media being converted into the space between the rotor and the case of the device, which may result in rotor drive overloads, the overheat of the structure and in the jamming of the rotor;the lack of the opportunity to introduce the second component in liquid form into the disperser for conversion, with intensive mixing of the components, disperse and mechanically activate them with their greater localized mass transfer;the lack of functionally connected adjustable rotor drive speeds and the regulation of mass feed of components for conversion to ensure the optimization of the modes of this conversion and to prevent the device from switching to cavitation mode by controlling acoustic noises in the media being converted.

The reasons impeding the technical result being obtained in comparison with the solutions for invention [81]:the relatively low reliability of the potential conversion of the reaction components of anomalously viscous flowing media due to the fact that a limited number of design and process elements (only two screws) are provided for it and there are no internal disintegrator cleaning devices;the lack of the opportunity to introduce the second component in liquid form into the device for conversion, with intensive mixing of the components, disperse and mechanically activate them with their greater localized mass transfer;the complexity and greater metal intensity of the electromechanical design of the disintegrator, including the need to use special electric motors with hollow rotors.

a) the lack of reliability or inability to convert the reaction components of anomalously viscous flowing media due to the following reasons:due to the fact that the crushing chamber is equipped with rotating brush-type cleaning devices located transversely to the rotor axis and according to their design arrangement in general, “dead” zones form in the crushing chamber (which is evident from the drawing) where incompletely reacted reaction components are accumulated, which may result in their “regular” discharge into the flow being processed, which results in the formation of chemically heterogeneous macro-fragments of the medium being converted at the outlet of the disintegrator;a probable possibility (depending on the viscosity and adhesion properties of the compositions being converted and / or their non-Newtonian liquid-type properties) of the accumulation of the incompletely reacted reaction components in the brush volumes of the cleaning devices, which results in their “regular” discharge into the flow being processed, which results in the formation of chemically heterogeneous macro-fragments of the medium being converted at the outlet of the disintegrator;

b) the lack of design blocking for the ingression of the compositions being processed and affected by centrifugal forces into the space between the rotors and the case of the disintegrator, which may result in the jamming of the rotor during the processing of high viscosity media; a “classical” hydraulic puller is used for the presented invention;

c) the lack of design and process reinforcement for the operating rotor rods, their strength and operating resource (rod diameters are increased along with the peripheral withdrawal of the rods from the rotor rotation axes due to the inevitable increase in the loads affecting them in the presented invention);

d) the lack of a regulated metering feed drive of the flow of the medium being converted to the disintegrator, including a screw assembly with anti-adhesive surfaces;

e) the lack of space-oriented surfaces of hydraulic valve openings with pumping and reflecting properties, the design elements ensuring the advancement of the medium being converted with the change in its direction—from that of loading / feeding the medium being converted into the disintegrator to that towards the crushing chamber, parallel to the rotor rotation axis;

f) the low reliability of the feed of a high viscosity medium being converted into the disintegrator due to the lack of an active concentric two-screw channel for feeding the medium being converted horizontally—into the crushing chamber;

j) the lack of control of the boundary of the potential shift of the disintegrator / reactor to cavitation mode by means of an acoustic sensor, which results in the lack of automatic stabilization of the operation mode in the sub-cavitation area;

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